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WO1983000184A1 - Centrifugal pump - Google Patents

Centrifugal pump Download PDF

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Publication number
WO1983000184A1
WO1983000184A1 PCT/US1982/000523 US8200523W WO8300184A1 WO 1983000184 A1 WO1983000184 A1 WO 1983000184A1 US 8200523 W US8200523 W US 8200523W WO 8300184 A1 WO8300184 A1 WO 8300184A1
Authority
WO
WIPO (PCT)
Prior art keywords
iron
centrifugal pump
housing
volute
pump according
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
PCT/US1982/000523
Other languages
French (fr)
Inventor
Inc. Turbine Metal Technology
George Kelly Sievers
Eugene V. Clark
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to AU85236/82A priority Critical patent/AU8523682A/en
Publication of WO1983000184A1 publication Critical patent/WO1983000184A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/60Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using solids, e.g. powders, pastes
    • C23C8/78Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using solids, e.g. powders, pastes more than one element being applied in more than one step
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/02Selection of particular materials
    • F04D29/026Selection of particular materials especially adapted for liquid pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D7/00Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts
    • F04D7/02Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type
    • F04D7/04Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2230/00Manufacture
    • F05D2230/90Coating; Surface treatment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2300/00Materials; Properties thereof
    • F05D2300/10Metals, alloys or intermetallic compounds
    • F05D2300/17Alloys
    • F05D2300/171Steel alloys
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2300/00Materials; Properties thereof
    • F05D2300/20Oxide or non-oxide ceramics
    • F05D2300/22Non-oxide ceramics
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2300/00Materials; Properties thereof
    • F05D2300/20Oxide or non-oxide ceramics
    • F05D2300/22Non-oxide ceramics
    • F05D2300/226Carbides

Definitions

  • This invention has to do with centrifugal pumps, and more particularly is concerned with centrifugal pumps having increased erosion wear resistance, enabling longer life in severe usage applications such as the pumping of finely particulate slurries, e.g. coal slurries.
  • Centrifugal pumps are well known apparatus for the pumping of fluids such as gases, liquids and suspensions by the rotation of an impeller within a volute.
  • the fluid to be pumped passes along a flow path extending from central inlet to the impeller, whence the fluid is exp.elled at a high rate centrifugally outward against a surrounding volute which opens to a horn leading to the pump outlet.
  • all parts of the pu ⁇ p housing and components are subjected to wear, particularly when- pumping finely particulate materials such as slurries or suspensions of coal, some. parts by virtue of their location are particularly subject to erosive wear, i.e.
  • the pump housing and pump components a re fabricated of steel , generally a carbon steel , and sometimes an iron base stainless steel.
  • Such pumps can be improved in erosion wear resistance in accordance with the invention.
  • the eros i on res i stance benefi ts conferred by the invention can be obtained loca l ly i n areas need ing them , so that the enti re pump need not be fabricated of exotic materials , nor coated enti rely wi th a special i zed coating which in fact is needed only here and there.
  • centrifugal pump It is therefore an object of the invention to provide a centrifugal pump. It is another object to provide a centrifugal pump having locally improved wear resistance. Another object is the provision of a pump and pump components which are locally and specifically improved in erosion wear resistance, particularly in the areas of the cutwater, the impeller, the wear rings and the volute, with a view to longer,- more reliable pump operation.
  • a centrifugal pump adapted for pumping finely particulate slurries, comprising a steel housing having an inlet and an outlet and a volute therebetween, a motor mounted on the housing, and an impeller rotatably driven within the volute by the motor for pumping fluid through the housing along a flow .path extending through the volute and between the inlet and outlet, the pump having surfaces conditioned against erosive wear along the flow path comprising iron carbide and iron boride formed in situ locally at pump steel surfaces subject to erosive wear.
  • the pump impeller is locally surface conditioned with iron carbide and iron boride;
  • the volute includes a cutwater, and the cutwater is locally surface conditioned with the iron carbide and iron boride;
  • the impeller is mounted in the housing with steel wear rings, and the wear rings are locally surface conditioned with the iron carbide and iron boride; and
  • the steel housing comprises carbon steel or iron base stainless steel.
  • centrifugal pump in which the housing surfaces are coated with an erosion resistant coating comprising an inner layer of iron carbide and an outer layer of iron boride, and particularly wherein the outer layer of iron boride is iron carbide containing.
  • an erosion resistant coating comprising an inner layer of iron carbide and an outer layer of iron boride, and particularly wherein the outer layer of iron boride is iron carbide containing.
  • the pump coating is from 0.4 to 0.8 millimeter in depth, overall, and the outer layer of iron boride is from 0.5 to 0.06 millimeter in depth.
  • the coating is formed by first diffusing carbon locally into the pump surfaces to be conditioned then after the carbon diffusion, diffusing boron from a diffusion pack at elevated temperatures and in the absence of oxygen, and thereafter quenching, to define an iron cabide layer outwardly relatively rich in iron boride as the coating.
  • Fig. 1 is a view in vertical section of the present pump taken on line 1-1 in Fig. 2;
  • Fig. 2 is a view in horizontal section thereof, taken on line 2-2 in Fig. 1. .
  • a typical centrifugal pump is shown at 10, and comprise a steel housing 12 defining a horizontally deposed volute 14 in which impeller 16 rotates counter-clockwise driven by motor 18 on shaft 20 ' .
  • liquid, gas or slurry to be pumped enters the pump 10 centrally at inlet 26, is thrown outwardly by impeller vanes 28 into volute 14 whence it is collected, carried spirally, divided by cutwater 30 and ejected at outlet horn 32.
  • the surface to be conditioned is delineated and preferably subjected to a two step diffusion as follows:
  • the areas to be conditioned are carburized. Carbon from a carbon source such as a commercial carburizing compound, or methane, is diffused into the delineated areas by heating the area in contact with the carbon source, for a time, e.g. 5 hours and at a temperature,- e.g. 1625 F, at which a subsurface carbon diffusion and formation of iron carbides to a suitable depth e.g. 0.4 to 0.8 millimeter, is realized. Since the pump housing and components being conditioned are steel parts, e.g. carbon steel or iron base stainless steel, the iron carbides are formed in the treated surface locally and responsive to the carbon diffusion thereinto. As mentioned where carbonitriding is employed, e.g. using sodium cyanide as the carbonitriding agent, iron nitrides are obtained in the conditioned surface, along with iron carbides and iron borides.
  • a carbon source such as a commercial carburizing compound, or methane
  • the area to be conditioned, now carburized, is then subjected to a boron diffusion under conventional conditions of time, temperature, and in an oxygen-free environment from a diffusion pack of per se known
  • OMPI composition For example, the part having the preformed iron carbide surface is immersed in a boro-nizing pack having typically the composition by weight:
  • Halogen activator sufficient to activate the pack
  • the pack is heated at 1650 °F. for eight hours or until a diffusion of boron to a depth of about 0.5 to 0.06 millimeter is realized, the boron combining with the iron present in the part surface to form iron borides, in the presence of the iron carbides. Because of the sequencing of diffusion steps, the outer portion of the coating is relatively rich in iron borides, and the inner portion thereof comparatively richer in iron carbides. The iron carbides are present in. the outer predominantly iron boride layer as well, of course. The part is then quenched.
  • the result of the foregoing steps is a sequential iron carbide-iron boride modification of the part surface locally, corresponding to the portion or portions of the impeller,, volute, cutwater, wear rings and so on locally subjected to diffusion.
  • the portions to be treated are placed in the pack and the treatment carried out.
  • the thus locally conditioned portions or portion areas show exceptional resistance to wear by erosion, caused by innumerable low energy impacts of fine particulates with the surface areas. This result is unexpected in centrifugal pump applications since there appears to be no known theoretical basis for predicting or explaining the improvement obtained. For example.
  • the role of the iron carbide in the present invention is not clear, since from a theoretical viewpoint its presence should not result in substantial improvement of the iron boride diffusion coating. But surprisingly, there is a remarkably beneficial effect on the erosion characteristic of the coating with ' the iron carbide preformation.
  • the iron boride alone typically will last only 75% as long as the iron carbide/iron boride combination diffusion coating, in a like centrifugal pump application.
  • the iron carbide alone shows no improvement over the steel surface alone. A synergistic result therefore is obtained which was 'not predictable from a consideration of the component materials, prior to experimentation.
  • the invention thus provides a centrifugal pump apparatus which operates longer, has fewer failures from erosion, and which is an improved pump product over this type of pump as previously known.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Abstract

Centrifugal pump (10) adapted for pumping finely particulate slurries, comprising a steel housing (12) having an inlet (26) and an outlet (32) and a volute (14) therebetween, a motor (18) mounted on the housing (12) and an impeller (16) rotatably driven within the volute (14) by the motor (18) for pumping fluid through the housing (12) along a flow path extending through the volute (14) and between the inlet (26) and outlet (32) the pump (10) having surfaces conditioned against erosive wear along the flow path comprising iron carbide and iron boride formed in situ locally at pump steel surfaces subject to erosive wear.

Description

CENTRIFUGAL PUMP.
Technical Field-
This invention has to do with centrifugal pumps, and more particularly is concerned with centrifugal pumps having increased erosion wear resistance, enabling longer life in severe usage applications such as the pumping of finely particulate slurries, e.g. coal slurries.
Background Art #
Centrifugal pumps are well known apparatus for the pumping of fluids such as gases, liquids and suspensions by the rotation of an impeller within a volute. The fluid to be pumped passes along a flow path extending from central inlet to the impeller, whence the fluid is exp.elled at a high rate centrifugally outward against a surrounding volute which opens to a horn leading to the pump outlet. Although all parts of the puπp housing and components are subjected to wear, particularly when- pumping finely particulate materials such as slurries or suspensions of coal, some. parts by virtue of their location are particularly subject to erosive wear, i.e. wear caused not so much by large particle abrasion as by millions of minute contacts by the small particles which characterize fine particulate slurries. One area receiving considerable erosive contact is the cutwater, the sharply angled divider between the volute and the outlet horn; another area highly subject to erosion is on the wear rings on which the impeller turns; another is the impeller itself, the volute wall surrounding it, and •those other areas where particle impact is at relatively higher velocities or frequency.
Typically, the pump housing and pump components a re fabricated of steel , generally a carbon steel , and sometimes an iron base stainless steel. Such pumps can be improved in erosion wear resistance in accordance with the invention.
Impo rtantly , the eros i on res i stance benefi ts conferred by the invention can be obtained loca l ly i n areas need ing them , so that the enti re pump need not be fabricated of exotic materials , nor coated enti rely wi th a special i zed coating which in fact is needed only here and there.
*
Description of the Invention
It is therefore an object of the invention to provide a centrifugal pump. It is another object to provide a centrifugal pump having locally improved wear resistance. Another object is the provision of a pump and pump components which are locally and specifically improved in erosion wear resistance, particularly in the areas of the cutwater, the impeller, the wear rings and the volute, with a view to longer,- more reliable pump operation.
These and other objects of the invention to become apparent hereinafter are realized in a centrifugal pump adapted for pumping finely particulate slurries, comprising a steel housing having an inlet and an outlet and a volute therebetween, a motor mounted on the housing, and an impeller rotatably driven within the volute by the motor for pumping fluid through the housing along a flow .path extending through the volute and between the inlet and outlet, the pump having surfaces conditioned against erosive wear along the flow path comprising iron carbide and iron boride formed in situ locally at pump steel surfaces subject to erosive wear.
In particular embodiments of the invention, the pump impeller is locally surface conditioned with iron carbide and iron boride; the volute includes a cutwater, and the cutwater is locally surface conditioned with the iron carbide and iron boride; the impeller is mounted in the housing with steel wear rings, and the wear rings are locally surface conditioned with the iron carbide and iron boride; and the steel housing comprises carbon steel or iron base stainless steel.
In further embodiments of the invention, there is provided the mentioned centrifugal pump in which the housing surfaces are coated with an erosion resistant coating comprising an inner layer of iron carbide and an outer layer of iron boride, and particularly wherein the outer layer of iron boride is iron carbide containing. Where carbonitriding is used in advance of the boronizing step, iron nitrides are also formed in the conditioned surface, along with the iron borides and iron carbides.
In accordance with the invention, the pump coating is from 0.4 to 0.8 millimeter in depth, overall, and the outer layer of iron boride is from 0.5 to 0.06 millimeter in depth.
Preferably, in the centrifugal pump according to the invention, the coating is formed by first diffusing carbon locally into the pump surfaces to be conditioned then after the carbon diffusion, diffusing boron from a diffusion pack at elevated temperatures and in the absence of oxygen, and thereafter quenching, to define an iron cabide layer outwardly relatively rich in iron boride as the coating.
The Drawings
The invention will be further described as to an illustrative embodiment in conjunction with the attached drawings in which:
Fig. 1 is a view in vertical section of the present pump taken on line 1-1 in Fig. 2; and
Fig. 2 is a view in horizontal section thereof, taken on line 2-2 in Fig. 1. .
Preferred Modes
Turning now the drawings in detail, in Fig. 1 a typical centrifugal pump is shown at 10, and comprise a steel housing 12 defining a horizontally deposed volute 14 in which impeller 16 rotates counter-clockwise driven by motor 18 on shaft 20'. Upper and lower wear rings 22, 24, journal the impeller 16 in the housing 12. In operation, liquid, gas or slurry to be pumped enters the pump 10 centrally at inlet 26, is thrown outwardly by impeller vanes 28 into volute 14 whence it is collected, carried spirally, divided by cutwater 30 and ejected at outlet horn 32.
When pumping finely particulate slurries, several locations along the flow path are subjected to extraordinary erosion-. These include the inner and outer surfaces of the wear rings 22, 24 and the mating bearing surfaces of the impeller 16, the portions of the volute 14 impacted' by the slurry e.g. areas 34, the cutwater 30, and of course the flow directing portion of the impeller 16, e.g. areas 40, are typical areas benefitting by the localized surface conditioning of the invention.
To so surface condition these several areas, all or some of them, the surface to be conditioned is delineated and preferably subjected to a two step diffusion as follows:
The areas to be conditioned are carburized. Carbon from a carbon source such as a commercial carburizing compound, or methane, is diffused into the delineated areas by heating the area in contact with the carbon source, for a time, e.g. 5 hours and at a temperature,- e.g. 1625 F, at which a subsurface carbon diffusion and formation of iron carbides to a suitable depth e.g. 0.4 to 0.8 millimeter, is realized. Since the pump housing and components being conditioned are steel parts, e.g. carbon steel or iron base stainless steel, the iron carbides are formed in the treated surface locally and responsive to the carbon diffusion thereinto. As mentioned where carbonitriding is employed, e.g. using sodium cyanide as the carbonitriding agent, iron nitrides are obtained in the conditioned surface, along with iron carbides and iron borides.
The area to be conditioned, now carburized, is then subjected to a boron diffusion under conventional conditions of time, temperature, and in an oxygen-free environment from a diffusion pack of per se known
OMPI composition. For example, the part having the preformed iron carbide surface is immersed in a boro-nizing pack having typically the composition by weight:
Boron powder 2-10%;
Halogen activator sufficient to activate the pack;
Aluminum oxide, the balance. The pack is heated at 1650 °F. for eight hours or until a diffusion of boron to a depth of about 0.5 to 0.06 millimeter is realized, the boron combining with the iron present in the part surface to form iron borides, in the presence of the iron carbides. Because of the sequencing of diffusion steps, the outer portion of the coating is relatively rich in iron borides, and the inner portion thereof comparatively richer in iron carbides. The iron carbides are present in. the outer predominantly iron boride layer as well, of course. The part is then quenched. The result of the foregoing steps is a sequential iron carbide-iron boride modification of the part surface locally, corresponding to the portion or portions of the impeller,, volute, cutwater, wear rings and so on locally subjected to diffusion. The portions to be treated are placed in the pack and the treatment carried out. The thus locally conditioned portions or portion areas show exceptional resistance to wear by erosion, caused by innumerable low energy impacts of fine particulates with the surface areas. This result is unexpected in centrifugal pump applications since there appears to be no known theoretical basis for predicting or explaining the improvement obtained. For example.
OMPI conventional theories of support for a fragile coating as enhancing the performance of the coating would not seem to apply in the pump art where the impacts are minute, not heavy, and numerous, not infrequent. While not wishing to be bound to any particular theory, it is believed that the energy levels of the multitudinous impacts being low but continuous act to strip from the non-coated surface atoms needed to keep the surface from eroding, and the formation of the presently described coating blocks this action, effecting the noted improvements.
The role of the iron carbide in the present invention is not clear, since from a theoretical viewpoint its presence should not result in substantial improvement of the iron boride diffusion coating. But surprisingly, there is a remarkably beneficial effect on the erosion characteristic of the coating with' the iron carbide preformation. For example the iron boride alone typically will last only 75% as long as the iron carbide/iron boride combination diffusion coating, in a like centrifugal pump application. The iron carbide alone shows no improvement over the steel surface alone. A synergistic result therefore is obtained which was 'not predictable from a consideration of the component materials, prior to experimentation.
The invention thus provides a centrifugal pump apparatus which operates longer, has fewer failures from erosion, and which is an improved pump product over this type of pump as previously known.

Claims

Claims
1. Centrifugal pump adapted for pumping- finely particulate slurries, comprising a steel housing having an inlet and an outlet and a volute therebetween, a motor mounted on said housing, and an impeller rotatably driven within the volute by said motor for pumping fluid through said housing along a flow path extending through said volute and between said inlet and outlet, said pump having surfaces conditioned against erosive wear along said flow path comprising iron carbide and iron boride formed in situ locally at pump steel surfaces subject to erosive wear.
2. Centrifugal pump -according to claim 1, in which" said impeller is locally surface conditioned with iron carbide and iron boride.
3. Centrifugal pump according to claim 1, in- which said volute includes a cutwater, said cutwater being locally surface conditioned with said iron carbide and iron boride.
4. Centrifugal pump according to claim 1, in which said impeller is mounted in said housing with wear rings, said wear rings being locally surface conditioned with said iron carbide and boron carbide.
5. Centrifugal pump according to claim 1 in which said steel housing comprises carbon steel.
6. • Centrifugal pump according to claim 1, in which said steel housing comprises iron base stainless steel.
7» Centrifugal pump according to claim 1,* in which said conditioned surfaces further comprise iron nitride produced by carbonitriding said surfaces.
8. Centrifugal pump according to claim 1, in which pump surfaces are coated with an erosion resistant coating comprising an inner layer of iron carbide and an outer layer of iron boride.
9. Centrifugal pump ccording to claim 8, in which said outer layer of iron boride is iron carbide containing.
10. Centrifugal pump according to claim 9, in which said coating is from 0.4 to 0.8 millimeter in depth.
11. Centrifugal pump according to claim 10, in which said coating outer layer of iron boride is from 0.5 to 0.06 millimeter in depth.
12. Centrifugal pump according to claim 11, in which said coating is formed by first diffusing carbon locally into said pump housing surface, then after the carbon diffusing boron from a diffusion pack at elevated temperatures and in the absence of oxygen, and thereafter : quenching, to define an iron carbide layer outwardly relatively rich in iron boride as the coating.
w
PCT/US1982/000523 1981-07-02 1982-04-22 Centrifugal pump Ceased WO1983000184A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU85236/82A AU8523682A (en) 1981-07-02 1982-04-22 Centrifugal pump

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US279,828810702 1981-07-02
US06/279,828 US4826401A (en) 1981-07-02 1981-07-02 Centrifugal pump

Publications (1)

Publication Number Publication Date
WO1983000184A1 true WO1983000184A1 (en) 1983-01-20

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1982/000523 Ceased WO1983000184A1 (en) 1981-07-02 1982-04-22 Centrifugal pump

Country Status (3)

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US (1) US4826401A (en)
EP (1) EP0082850A1 (en)
WO (1) WO1983000184A1 (en)

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US5290236A (en) * 1991-09-25 1994-03-01 Baxter International Inc. Low priming volume centrifugal blood pump
US5263924A (en) * 1991-09-25 1993-11-23 Baxter International Inc. Integrated low priming volume centrifugal pump and membrane oxygenator
US5393207A (en) * 1993-01-21 1995-02-28 Nimbus, Inc. Blood pump with disposable rotor assembly
US6187147B1 (en) 1998-05-15 2001-02-13 Conoco Inc. Delayed coker unit furnace
US6220234B1 (en) 1999-03-04 2001-04-24 Cummins Engine Company Coated compressor diffuser
US6398494B1 (en) * 1999-05-14 2002-06-04 Argo-Tech Corporation Centrifugal pump impeller
US7044288B2 (en) * 2002-04-09 2006-05-16 K-Tron Technologies, Inc. Bulk material pump feeder with reduced disk jamming
US6832887B2 (en) * 2002-04-09 2004-12-21 K-Tron Technologies, Inc. Bulk material pump feeder
JP5478067B2 (en) * 2005-10-12 2014-04-23 ケイ−トロン・テクノロジーズ・インコーポレイテッド Bulk material pump feeder with reduced disk jam, elastic disk
US9737933B2 (en) 2012-09-28 2017-08-22 General Electric Company Process of fabricating a shield and process of preparing a component
US9739284B2 (en) * 2013-11-19 2017-08-22 Charles Wayne Zimmerman Two piece impeller centrifugal pump
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US12338826B2 (en) * 2022-02-23 2025-06-24 Mirna Elnar Universal spa pump

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EP0082850A1 (en) 1983-07-06
US4826401A (en) 1989-05-02

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